JP5532286B2 - Fluid processing equipment - Google Patents

Description

  The present invention relates to a fluid processing apparatus that performs fluid processing such as sterilization, deodorization, low molecular weight, activation, and deterioration prevention of fluids such as water, air, gas, and fuel oil by utilizing the ionizing action of α particle beam.

Conventionally, an α-ray emitter having an α-ray emitting material that emits α-particle beams (helium atoms) is provided inside a frame body that uses an internal space as a fluid flow path from an inlet to an outlet. As a fluid processing apparatus that performs fluid processing by irradiating and ionizing an α particle beam (hereinafter simply referred to as an α ray), those having configurations shown in Patent Document 1 and Patent Document 2 are already known.
The α-ray radiator of the above-mentioned Patent Document 1 is a piezoelectric phenomenon in which barleystone powder is mainly mixed with crystal powder, titanium oxide powder, aluminum silicate compound powder, etc. with a binder, granulated to a particle size of about 5 mm and fired. A hard granular material showing an α-ray granular radiator by attaching thorium oxide to the surface of the granular body, and a plurality of α-ray granular radiators are arranged on a net-like holding member with a spacing adjacent to each other. The configuration is set.
In addition, the α-ray radiator according to Patent Document 2 has a high irradiation action efficiency by converting an α-ray radiation material made of thorium oxide into an α-ray radiation ceramic through a fixing layer on a holding core material that enables fluid flow. It has a configuration.

All of the above α-ray emitters change the molecular structure of air, gas, oil, water, etc. by causing ionization of fluid molecules and artificial conversion of nuclei by the large ionization action of α-rays. That, in the water strongly turned into ions, sterilization of efficient water, deodorization, decoloration or the like is performed. Similarly, for the air, for example, artificial conversion of the nuclei of air molecules represented by the following equation based on Rutherford's theory is generated, and combustion efficiency is improved, deodorization, sterilization of airborne bacteria, and the like are performed. In addition, ion activation, deterioration prevention, and the like can be performed for oils, and in fuel oil, combustion efficiency can be improved by making small molecules by breaking carbon molecular bonds and radicalization.

  The fluid processing apparatuses according to Patent Documents 1 and 2 are characterized by ionizing the fluid molecules that collide with the α-rays by ionization and various modifications to achieve the desired effect. Since there is a restriction on the dose of α rays and the effective radiation distance, there is a problem that α molecules cannot be efficiently irradiated to fluid molecules flowing from the upstream side to the downstream side in the flow direction in the frame. For this reason, it is attempted to coat a large amount of α-ray radiation material on a holding member such as a holding core material or a granular material. In this case, however, a large amount of α-ray radiation material is required, which increases the cost of the apparatus. At the same time, there arises a manufacturing problem such that it is difficult to coat the holding member with the α-ray radiation material thickly.

On the other hand, when the α-ray emitting material is coated on a holding member with a large surface area or a net-like holding member with a small mesh, the α dose can be secured even if the α-ray emitting material is thinly coated. There is a problem that the flow resistance of the α-ray radiator installed in the direction intersecting the flow direction in the frame is increased.
In order to solve the above-mentioned problems, the present invention provides a fluid processing apparatus capable of improving the irradiation efficiency of α rays by an α ray emitter by activating the molecular motion of the fluid circulating in the frame. is there.

In the fluid processing apparatus for solving the above-mentioned problems, first, α-ray radiation that emits α-rays is formed inside the frame 4 that uses the internal space as a fluid flow path from the inlet 14 toward the outlet 16. In the fluid processing apparatus 1 that performs the fluid processing by providing the α-ray radiator 2 provided with the material and ionizing the fluid by irradiating the fluid with α-rays, the frame body 4 activates the molecular motion of the fluid. The unit 3 is provided, and the fluid subjected to the molecular motion activation by the molecular motion promoting unit 3 is irradiated with α-rays to perform fluid treatment, and the α-ray radiator 2 is provided upstream of the filter 17 provided in the frame 4 or Provided close to the downstream side , the fluid treatment device 1 is installed in the exhaust passage of the combustion device 35, and is connected to the upstream side fluid treatment device 1a installed in the exhaust passage as the fluid treatment device 1 and the exhaust passage. A downstream fluid treatment device 1b is provided, and an upstream fluid treatment device 1 is provided. The outlet 16 is connected to the frame 4 of the downstream fluid processing apparatus 1b, and the processing fluid processed by the upstream fluid processing apparatus 1a is supplied to the fluid flowing through the frame 4 of the downstream fluid processing apparatus 1b. A burner device 36 for supplying high-temperature energy into the exhaust passage is provided upstream of a supply portion to which the processing fluid is supplied to the downstream fluid processing device 1b .

  Secondly, the α-ray radiator 2 is an α-ray granular radiator 2a made of a granular material coated with an α-ray radiation material, and a large number of α-ray granular radiators 2a are moved into the frame 4 and fluid flows. It is characterized by being configured to be filled as possible.

Thirdly, the α-ray radiator 2 is supported in a rotatable manner within the frame body 4.

  Fourth, the molecular motion promoting unit 3 is characterized by being an ultrasonic wave generating unit 7 that generates ultrasonic waves toward the α-ray emitter 2.

  Fifth, the molecular motion promoting unit 3 is characterized by being a magnetic generating unit 6 that generates magnetic lines of force toward the α-ray radiator 2.

  Sixth, the present invention is characterized in that the frame 4 is provided with a fluid supply nozzle 31 for supplying another fluid to the fluid flowing inside.

  Seventh, the frame 4 is characterized in that a mist supply pipe 23 is provided for supplying mist to the fluid flowing through the inside on the upstream side or the downstream side of the α-ray radiator 2.

The fluid processing apparatus configured as described above can achieve the following effects. According to the first aspect of the present invention, the molecular motion activation energy generated by the molecular motion promoting portion activates the molecular motion of the fluid and ionizes the molecule, and the α-ray emitted from the α-ray emitter is emitted to the excited fluid. By irradiating, it is possible to increase the irradiation efficiency, bring more fluid molecules and nuclei into contact with α-rays, promote ionization, and efficiently perform fluid treatment.
This brings about effects such as purification of air, gas, water, and oil, improvement of quality function, prevention of deterioration, activation, and improvement of fuel combustion efficiency, and a simple and inexpensive configuration of the fluid treatment device. can do. Further, by bringing the α-ray radiator close to the upstream side or the downstream side of the filter, the α-ray radiator can be easily installed using the filter or the filter mounting structure.
In addition, the outlet is connected to the frame of the downstream fluid processing apparatus, and the processing fluid processed by the upstream fluid processing apparatus is supplied to the fluid flowing through the frame of the downstream fluid processing apparatus, and the upstream fluid By providing a burner device 36 for supplying high temperature energy into the chimney of the combustion device 35 for burning various fuels upstream of the supply portion of the processing fluid processed by the processing device 1a, the downstream fluid processing device The high-temperature energy supplied by the burner device upstream of the frame body allows, for example, the tar content in the exhaust gas flowing in the chimney to be burned and removed in advance, and then the exhaust gas treatment by the upstream fluid treatment device can be performed efficiently.

  According to the second aspect of the present invention, each α-ray granular radiator is moved and distributed in the frame and is in a state of being laminated so that fluid molecules are repeatedly brought into contact with the surface of the granular material to circulate the fluid. Processing can be facilitated.

  According to the invention of claim 3, by operating the α-ray emitter in the frame body, the α-rays radiated from the α-ray emitter can be efficiently brought into contact with the circulating fluid molecules, and fluid processing can be promoted. it can.

According to the invention of claim 4, since the ultrasonic wave generation unit generates the ultrasonic wave toward the α-ray emitter side, the fluid treatment can be efficiently performed by activating the fluid molecules to increase the irradiation efficiency by the α-rays. In addition, the ultrasonic generator can be installed at an appropriate position of the frame body in a space-saving manner, and can be easily retrofitted to a utilization device such as an air cleaner.

According to the invention of claim 5, the magnetism generating section generates magnetic lines of force toward the α-ray emitter side and activates fluid molecules by activating the magnetic energy, so that it is possible to increase the irradiation efficiency by α-rays and efficiently perform fluid processing. To. Further, the magnetism generator can be easily installed at an appropriate position of the frame.
In addition, when the magnetism generating unit is an AC type that generates magnetic force lines by AC electricity, fluid molecules are more activated by the magnetic field energy that changes the direction, so that it is possible to promote fluid processing with higher irradiation efficiency by α rays. .

According to the sixth aspect of the present invention, it is possible to easily supply another fluid from the fluid supply nozzle to the fluid in the frame, and to perform fluid processing in which a plurality of fluids are mixed.
As a result, another fluid supplied into the frame can be ionized by ionizing with α rays emitted from the α-ray radiator and mixed with the processing fluid in the frame, and the mixed processing fluid can be mixed with the engine or combustion furnace. , And can be supplied to various utilization devices such as chemical synthesis devices.

According to the seventh aspect of the present invention, it is possible to easily supply the mist from the mist supply pipe to the fluid in the frame body, and it is possible to perform the fluid processing in which the mist is mixed with the fluid. As a result, when the mist supplied into the frame is ionized by α rays emitted from the α ray emitter, the ionized mist and the processed fluid can be easily mixed.

  An embodiment of the present invention will be described with reference to the drawings. 1 to 10, reference numeral 1 denotes a fluid processing apparatus that performs fluid processing by providing an α-ray radiator 2 and a molecular motion promoting unit 3 in a frame 4 that forms a fluid processing channel (processing chamber). . The α-ray radiator 2 used in this embodiment is configured to radiate radiant energy of thorium oxide based on the techniques disclosed in Patent Documents 1 and 2 with an α particle beam of about 4.01 to 10 MeV. As a result, the α-ray emitter 2 collides (contacts) the α-rays with the molecules or nuclei constituting the fluid by a known action when the α-rays to be emitted are irradiated with a fluid such as air, water, or oil as a workpiece. It is possible to perform ionization (ion activation) and fluid treatment (modification).

When air is irradiated with alpha rays, the ionization action of air molecules is enhanced and promoted by alpha rays, so that nitrogen (N), which occupies about 79.7% in the air, is converted into hydrogen (H) by an artificial nuclear conversion action. And water (H ₂ O) in the air are changed to hydrogen ions (H ⁺ ) and hydroxyl groups (OH ⁻ ). As a result, the air is artificially changed into a combustible material, and complete combustion operation becomes possible when the air is supplied to the internal combustion engine and various combustion devices together with the fuel oil for combustion. Therefore, even if the fuel supply valve is squeezed, the desired combustion energy can be sufficiently obtained, and the amount of fuel oil consumption can be reduced easily. Moreover, harmful components can be reduced with respect to the exhaust gas, and α rays modify the components of the gas for various gases.

In addition, when the oil is irradiated with α-rays, the carbon (C) bond in the oil is cleaved to reduce the molecular weight, and an oil that is easy to vaporize can be obtained and combustion can be promoted.
In addition, when water is irradiated with α rays, water (H ₂ O) is changed into hydrogen ions (H ⁺ ) and hydroxyl groups (OH ⁻ ), and at the same time, hydrogen peroxide (H ₂ O depending on the amount of dissolved oxygen). ₂ ) can be generated. Thereby, water can be modified into functional water having sterilizing power by fluid treatment with α rays.

On the other hand, the molecular motion promoting unit 3 is connected to a frame 4 that guides fluid from the upstream side to the downstream side in the flow direction (processing direction). It can be configured by providing any of the high-frequency generators or the like in combination.
The molecular motion activation energy generated by the molecular motion promoting unit 3 (hereinafter simply referred to as kinetic energy) is the activation of molecular motion of the fluid flowing through the frame 4 and the ionization of molecules (hereinafter simply referred to as molecular motion activity and To the excited state.

That is, since the fluid molecules are activated in the flow direction (Y direction), the lateral direction (X direction), and the molecular motion in the synthesis direction, α is emitted qualitatively from the motion-activated fluid molecules and the α-ray emitting material. The irradiation rate at which the lines can contact (collision) with each other is greatly increased. As a result, even if the fluid flows in a certain direction, it is possible to further promote ionization of the molecules and artificial conversion of nuclei.
Accordingly, the molecules are dispersed and accelerated so as to impart lateral movement (molecular movement activity) to the α-ray radiator 2 and the fluid flowing in a certain direction toward the emitted α-rays. However, since the α-rays can be brought into strong contact with each other, ionization of fluid molecules by the α-rays can be promoted and fluid treatment can be performed efficiently.

  Next, with reference to FIGS. 1-3, the fluid processing apparatus 1 concerning the 1st, 2nd, 3rd embodiment provided with the said alpha ray radiator 2 and the molecular motion promotion part 3 and its usage condition are demonstrated. First, in the fluid processing apparatus 1 according to the first embodiment shown in FIG. 2, the cleaner case of the air cleaner 13 provided on the upstream side of the vaporizer 12 a included in the engine 12 of the automobile 11 is a frame (processing cylinder) 4. . And the apparatus is comprised by providing the alpha ray radiator 2 and the molecular motion promotion part 3 in the said process cylinder 4 between the inflow port 14 and the sending / outlet port 16 which are formed in the both ends.

  The fluid processing apparatus 1 in the illustrated example is detachable in a state where the net-type α-ray radiator 2 is detachably mounted in the processing cylinder 4 and faces both the upstream and downstream filter surfaces of the air filter 17. Provided. The molecular motion promoting unit 3 is formed as an ultrasonic wave generating unit 7 that oscillates ultrasonic waves, and is provided so as to oscillate ultrasonic waves toward the α-ray radiator 2 installed on the upstream side of the air cleaner 13. The ultrasonic generator 7 preferably emits ultrasonic waves at a level of 20,000 to 250,000 Hz as a specification that has sufficient molecular motion activity and is commercially available and easy to adopt.

  In addition, the ultrasonic wave generation unit 7 is mounted on the automobile 11 so that the position of the oscillation head can be adjusted to the mounting unit 7a provided on the lower wall of the processing cylinder 4 so that the distance or orientation with respect to the α-ray radiator 2 can be adjusted. A main switch 19 and an ultrasonic generator 21 are provided and connected to a battery (power source) 18 to be connected. In the embodiment, the main switch 19 is operated in cooperation with a starter switch (not shown) installed in the control unit of the automobile 11.

  The ultrasonic generator 7 in the illustrated example is bent with respect to the α-ray radiator 2 having a size and shape that substantially covers the filter surface of the filter (air filter) 17 with the inlet 14 side facing the side. The ultrasonic wave emitted to the air on the upstream side of the α-ray radiator 2 can be provided substantially uniformly. As a result, the ultrasonic wave generation unit 7 activates the molecular motion of the air by ultrasonic waves on the upstream side of the air filter 17, and promotes contact with the α rays when the air molecules pass through the α ray emitter 2. Note that the necessary number of ultrasonic generators 7 can be provided on the upper wall bent sideward if necessary, or on the side wall (peripheral wall) of the processing tube 4.

With this configuration, the engine 12 of the automobile 11 converts the outside air (air) sucked from the inlet 14 of the fluid processing apparatus 1 into the ultrasonic generator 7, the first α-ray radiator 2, the air filter 17, and the second α. It is operated by passing the line radiator 2 and supplying it to the combustion chamber.
At this time, since the ultrasonic energy is applied to the air upstream of the α-ray radiator 2 by the ultrasonic generator 7, the molecular motion is activated and the molecules are ionized, and α-rays are generated in more nitrogen nuclei. Collisions are likely to occur, causing many artificial transformations of nuclei, producing a large amount of hydrogen, oxygen, and the like.

The treated air thus fluid-treated can be mixed with fuel oil in the vaporizer 12a to promote complete combustion and improve combustion efficiency.
Also as they may release minute contact hydrogen and hydroxyl and water likewise α line in the air, while reducing the consumption of fuel oil to enhance more the combustion efficiency, clean by reducing the harmful components in the exhaust gas exhaust Can be discharged as.

  And the fluid processing apparatus 1 of the example of illustration passes the alpha ray radiator 2 installed in the downstream of the air filter 17 after filtering the air which passed the air filter 17 after having processed the primary fluid as mentioned above. Then, irradiation with α rays can be further performed immediately before the combustion chamber. Therefore, in order to send the air whose fluid treatment is further promoted in conjunction with the primary fluid treatment to the combustion chamber, the combustion efficiency of the engine 12 is further enhanced, complete combustion is promoted, fuel consumption is reduced, and exhaust gas is purified. There is a feature that it can be made more effective.

  In addition, since the capability and shape of the air filter 17 are determined for each engine, when the α-ray radiator 2 is installed using the structure of the air cleaner 13, the number of the α-ray radiator 2 is installed. The shape and size of the air cleaner 13 are set according to the shape and the inflow amount of the air cleaner 13. Further, the fluid processing apparatus 1 in the illustrated example is installed by holding two air-permeable mesh-like α-ray radiators 2 on the air filter 17 side so as to intersect the air flow direction and partition the upstream side and the downstream side. However, the α-ray radiator 2 can be provided as a single sheet in order to reduce the internal air flow resistance, and can be installed either upstream or downstream of the air filter 17.

  Next, with reference to FIG. 3, the fluid processing apparatus 1 in connection with 2nd Embodiment and its usage example are demonstrated. In the following embodiments, descriptions of the same configurations and operations as those of the above-described embodiments will be omitted. The air cleaner 13 in the illustrated example has the α-ray radiator 2 facing the air filter 17 in the same manner as in the first embodiment, and the AC motion generator 6 generates magnetism by AC electricity in the molecular motion promoting unit 3. I have to. This magnetism generator 6 is attached to the processing cylinder 4 with a predetermined width so as to surround the outer periphery of the α-ray radiator 2 and is connected to the power source 18 via the main switch 19 and the AC modulation magnetic field generator 21a. . The magnetism generator 6 is provided along the processing cylinder 4 so that the position thereof can be adjusted, and the generated magnetic force can be adjusted by the AC modulation magnetic field generator 21a.

  In the fluid processing apparatus 1 configured as described above, when the main switch 19 is in the ON state and the starter switch is turned on, the engine 12 is started, the magnetism generating unit 6 generates magnetism when energized, and enters the flow path from the outer periphery of the processing cylinder 4. An alternating magnetic field is formed. As a result, the α-ray radiator 2 can be placed in the magnetic field, and movement of air molecules is activated by the magnetic energy in the air that reaches the α-ray radiator 2, and fluid processing by α-ray irradiation is promoted.

At this time, since the magnetism generator 6 instantaneously changes the direction of the magnetic field by AC electricity, the air molecules can be brought into an excited state in which the molecular motion is more activated by the magnetic force that changes the state of the magnetic field violently. Thereby, the ionization efficiency of air by α rays can be increased as compared with the case of using a permanent magnet, for example.
Further, since the magnetism generator 6 does not have an operating part like the ultrasound generator 7, the durability of the apparatus can be increased, and maintenance work can be saved. Moreover, since the magnetism generating unit 6 can be easily provided outside the processing cylinder 4, the retrofitting operation of the fluid processing apparatus 1 can be facilitated even for an engine 12 such as an existing automobile. Further, since the magnetism generating unit 6 does not directly contact the air (fluid) flowing in the processing cylinder 4, it is possible to prevent the fluid from being contaminated or to be worn early and to improve the durability.

  Note that the processing cylinder 4 is not limited to the AC-type magnetism generating section 6 but may be provided with a permanent magnet-type magnetism generating section 6. Further, as indicated by a dotted line, a plurality of permanent magnets can be provided in the processing cylinder 4 so as to intersect the flow direction with a flow interval. In this case, if the adjacent permanent magnets are provided with the same poles facing each other, the molecular motion activity can be further enhanced by the repulsive magnetic force.

The AC-type magnetic generator 6 and the permanent-magnet-type magnet generator 6 may be provided side by side. In this case, when the magnetic field generated by the AC-type magnet generator 6 is restricted, the restriction portion Can be easily supplemented by the magnet generator 6 of the permanent magnet type. Furthermore, since the ultrasonic generator 7 can also be easily installed in the processing cylinder 4, it is possible to easily compensate for the molecular motion activity at a required location, and the fluid processing device 1 adapted to a large engine or various combustion devices. Can be.

Next, with reference to FIG. 4, the fluid processing apparatus 1 in connection with 3rd Embodiment and its usage example are demonstrated. In this example, in the air cleaner 13 having the same α-ray radiator 2, the magnetic generator 6 and the air filter 17 as in the second embodiment, a mist generator is provided on a part of the processing cylinder 4 on the downstream side of the air filter 17. The fluid processing apparatus 1 is provided with 22 mist supply pipes 23.
The mist generating device 22 includes a mist generating section 24 and a supply section 26 that supplies a mist material into the mist generating section 24. From the mist supply pipe 23 that covers the mist generated in the mist generating section 24 with a heat insulating member. , Can be supplied into the processing cylinder 4 and supplied to the engine 12.

In the mist generator 22 of the illustrated example, the mist generator 24 is a tank in which the base of the mist supply pipe 23 is provided at the top, and the bottom of the tank is attached to the exhaust pipe 25 of the engine 12. As a result, water is supplied dropwise from the supply unit 26, evaporated by heat transfer through the exhaust pipe 25 that becomes high temperature, and the generated water vapor (mist) can be supplied to the processing cylinder 4 through the mist supply pipe 23. .
The fluid processing apparatus 1 including the mist generating device 22 having the above-described configuration is configured such that the mist supplied from the mist supply pipe 23 is merged with the processing air processed in the same manner as the above embodiment on the upstream side and mixed. Mixed air can be supplied to the engine 12.

  At this time, the water molecules of the mist irradiated with α-rays are ionized by irradiation with the processing air or α-rays and become hydrogen (H) and oxygen (O) and change into combustibles. Mix with garlic oil to promote combustion. Therefore, the fluid processing apparatus 1 including the mist generating device 22 can promote complete combustion of the fuel, can significantly reduce the fuel consumption of the engine, and can produce clean exhaust gas. At this time, if the mist is supplied in the form of a tornado (vortex) by the supply direction restricting means or the supply guide structure, the mist mixed air can be accelerated to further improve the combustion efficiency.

Further, the α-ray radiator 2 can be provided downstream of the supply port of the mist supply pipe 23 as indicated by a dotted line. In this case, since the mist can be directly irradiated with α rays, the ionization of water molecules can be further promoted. At this time, the net-like α-ray radiator 2 crosses the air flow direction according to the shape in the processing cylinder 4 and is installed so as to partition the upstream side and the downstream side. Can be efficiently irradiated with α rays.
The provision of the mist supply pipe 23 on the downstream side of the air filter 17 has an advantage that the air filter 17 is not wetted by the large mist.

  In addition, the engine 12 in the illustrated example is reformed by preliminarily treating the fuel oil by providing a fluid treatment device 1 for fuel treatment as will be described later with reference to FIG. 9 in addition to the fluid treatment device 1 for air treatment. The treated fuel oil is supplied to the engine 12. According to this, both air and fuel oil are fluid-processed and reformed, so that improvement in combustion efficiency, fuel consumption, and the like can be improved with a synergistic effect.

The mist generating device 22 is not limited to the exhaust pipe 25 and can be provided at an arbitrary location heated by the engine 12. In addition to the water vapor generating type, the mist generating / supplying means may be a means for misting the liquid using, for example, an ultrasonic wave generating element.
Further, when the fluid processing apparatus 1 as described above is used for gas or liquid processing in, for example, exhaust gas processing or chemical plants, the mist generating device 22 supplies not only water but also mist or chemical liquid. You can also.

  When the fluid processing apparatus 1 is used for an air cleaner 13 of a large engine such as a truck or a ship, the air cleaner 13 is generally provided with an air filter 17 formed in a cylindrical shape inside a cylindrical drum-shaped processing cylinder 4. However, using this structure, for example, a net-like α-ray radiator 2 is attached to be wound around the air filter 17 in a space formed between the air filter 17 and the processing cylinder 4, and the processing cylinder is used. It is desirable to provide the molecular motion promoting portion 3 on the outer periphery of 4. At this time, since the capacity and shape of the air filter 17 are determined for each engine, the number, shape, and size of the α-ray radiator 2 are provided corresponding to the shape of the air cleaner 13, the filtering ability, and the like.

Next, with reference to FIG. 5 and FIG. 6, a fluid processing apparatus 1 and an example of use thereof according to the fourth embodiment will be described. The fluid processing apparatus 1 includes an air filter 17, a permanent magnet type magnetic generator 6, a rotary α-ray radiator 2, and a permanent magnet type magnetic generator 6 from the upstream side inside a cylindrical processing cylinder 4. A net-type α-ray radiator 2 and a protective net 24 are sequentially arranged.
The processing cylinder 4 is provided with an outer cover 26 that hermetically forms a space (fluid supply chamber) 25 having a predetermined interval on the outer periphery, and an inflow pipe 27 is connected to the inflow port 14 side, and the outflow to the outflow port 16 side. A tube 28 is connected. The air filter 17 can also be installed on the inlet 14 side as indicated by the dotted line, and can be removed if unnecessary.

In the processing cylinder 4, an AC type magnetic generator 6 is installed on the outer periphery where the α-ray radiator 2 is located, and an ultrasonic generator 7 is installed at a desired location if necessary. A mist supply pipe 23 of the generator 22 is provided, and a plurality of fluid supply nozzles 31 are provided.
The fluid supply chamber 25 can supply air, gas, or various liquids sent from the fluid supply device 30 disposed outside to an appropriate place in the processing cylinder 4 from each fluid supply nozzle 31.
The fluid supply device 30 has the same configuration as the fluid processing device 1 similar to that of the above-described embodiment or this embodiment, and supplies the air processed by the fluid processing device 1 into the processing cylinder 4.

  The α-ray radiator 2 is operated in a direction intersecting with the fluid flow direction in the processing cylinder 4 to promote contact between α-rays and air molecules. That is, the α-ray radiator 2 of the embodiment is a net-type blade body 2 a having a plurality of propeller shapes as shown in FIGS. 5 and 6B, and each blade body 2 a is along the center of the processing cylinder 4. The rotating shaft 32 supported in this manner is projected in the radial direction. The rotating shaft 32 in the illustrated example is rotatably supported by a shaft supporting portion 33 provided in a plurality of rod-shaped permanent magnet type magnetism generating portions 6 fixed in parallel in the transverse direction in the processing cylinder 4. ing.

Further, the plurality of blade bodies 2a have a predetermined interval in the axial center direction of the rotating shaft 32 and are erected while changing the phase of each blade body 2a around the shaft center, whereby the plurality of blade bodies 2a are distributed over the entire cross section of the processing cylinder 4. Each blade body 2a is faced in a direction view so that air is efficiently brought into contact with each α-ray radiator 2.
Therefore, the α-ray radiator 2 configured as described above rotates around the rotation shaft 32 by the combined force of each propeller-shaped blade body 2a receiving the air flow force (wind pressure). It is possible to perform fluid treatment that promotes contact, and to increase the number of blades 2a and increase fluid treatment capacity because flow resistance is not increased.

  The blade body 2a is not limited to a net-like one, but can be a twisted plate-like propeller body coated with an α-ray radiation material. Further, the α-ray radiator 2 composed of the blades 2a accelerates the fluid in the flow direction while stirring the fluid when the rotary shaft 32 is forcibly rotated by the rotation drive device, so that the fluid treatment with reduced flow resistance is performed. Can do. Further, the rotating α-ray radiator 2 prevents adhesion of dust or water droplets to be attached by centrifugal force, so that the irradiation action of α-rays can be maintained for a long time and laborious maintenance work such as cleaning can be saved.

In addition, the α-ray radiator 2 is not limited to the shape of the blade body 2a, but may be a spiral shape provided with, for example, an α-ray radiator, and in this case, along the spiral surface while air is circulated. Since the guide is used, the contact between the α-rays and the air molecules can be further promoted, and the air can be circulated by generating a vortex. Further, when the α-ray radiator 2 formed of a helical body is rotationally driven, the flow resistance can be reduced as compared with the case where the α-ray radiator 2 is fixedly supported, and the generation of vortex can be urged toward the downstream side to accelerate the flow. The rotating shaft 32 can be a constituent member of the magnetism generator 6. Further, the α-ray radiator 2 is not limited to the rotational operation as described above, and the fluid treatment is performed by efficiently contacting the α-rays with the fluid molecules by means of reciprocating operation or vibration in an arbitrary direction within the processing cylinder 4. be able to.

  In the fluid processing apparatus 1 configured as described above, air supplied from the outlet 16 side via the air filter 17 is activated by the permanent magnet type magnetism generating unit 6 on the most upstream side, and the molecular motion is activated. This is brought into contact with the α-rays emitted from the rotating α-ray radiator 2 to perform the primary fluid treatment. Next, the air subjected to the primary fluid treatment is subjected to the secondary fluid treatment in the above-described molecular motion active environment by receiving the magnetic field from the AC type magnetic generator 6 and the ultrasonic waves from the ultrasonic generator 7, and further to the most downstream side. When passing through the installed net-like α-ray radiator 2, the tertiary fluid is processed and transferred from the outlet 16 to the outlet pipe 28. The mist supplied from the mist supply pipe 23 as needed is also efficiently fluid-treated while being mixed with air.

As a result, both the air and the mist can be efficiently processed in the same processing cylinder 4 and supplied to various utilization devices such as an engine, a combustion furnace, and a chemical synthesis device (not shown) in a homogeneous mixed state. .
In addition, the fluid processing apparatus 1 of the embodiment can replenish air at a proper position in the processing cylinder 4 via the fluid supply nozzle 31 or easily replenish the processing air or gas processed by the fluid supply apparatus 30. it can. Therefore, the gas and liquid required by the various utilization devices can be simultaneously supplied to the processing cylinder 4 to efficiently perform the fluid processing together with the air processing.

In addition, since the fluid processing apparatus 1 performs fluid processing by simultaneously mixing various fluids so that a variety of fluids can be supplied, the processing fluid is not limited to combustion, but can be obtained by using an air purification device, an exhaust gas processing device, and alpha rays. There is a feature that the use can be expanded as a manufacturing apparatus such as a chemical synthesis plant that performs ionization of a plurality of molecules into individual molecules, a pretreatment apparatus, and the like. In the various utilization devices as described above, the fluid processing apparatus 1 can easily attach a superheated part for heating the fluid and a cooling part for cooling the fluid to a desired place if necessary, so that various fluid treatments can be performed with high performance and low cost. Can be done.

  Next, with reference to FIG. 7, FIG. 8, the fluid processing apparatus 1 concerning 5th Embodiment and its usage example are demonstrated. The fluid processing apparatus 1 according to this embodiment shows an example in which the combustion apparatus 35 that burns various fuels such as oil, coal, and wood is installed in an exhaust path (such as a chimney) that discharges the exhaust gas. According to this example, the exhaust gas can be fluid-processed by the α-ray radiator 2 to make harmful components harmless or to be harmless, and it can be configured with high performance and low cost.

  The exhaust gas treatment apparatus 1 in the illustrated example includes a combustion pipe 37 that supplies high-temperature energy (fire flame, high-temperature air, etc.) generated by the burner device 36 into the chimney from the upstream side in the flow direction of the exhaust gas in the middle of the chimney, A fluid supply nozzle 31 of an upstream fluid treatment device 1a, which is a fluid supply device 30 similar to the above, is provided in the chimney, and the downstream fluid treatment device 1b is provided on the most downstream side thereof. Further, a cap-shaped cover 28a for preventing rainwater from entering is provided at the exhaust port of the chimney, and a net-type α-ray radiator 2 formed in a cylindrical shape is attached between the cover 28a and the exhaust port.

The burner device 36 of the exhaust gas treatment device 1 performs a primary exhaust gas treatment of the exhaust gas that burns the tar content in the exhaust gas and performs the tar treatment in order to supply the thermal power generated in the burner portion into the chimney through the combustion pipe 37. As a result, the burner device 36 efficiently performs the tar treatment while reducing the treatment load of the exhaust gas treatment (fluid treatment) by the fluid treatment device 1b installed on the downstream side. Preventing an increase or the like.
At this time, if the vortex guide wall 38 is formed in the inflow pipe 27 and the flame supplied from the combustion pipe 37 is guided in a spiral shape, the combustion gas can be generated in a tornado shape toward the downstream side. The combustion can be further promoted, the tar treatment efficiency can be further improved, and the exhaust can be made smoother.

The fluid supply device 30 supplies the treated air that has been previously treated with the α-ray radiator 2 by the upstream fluid treatment device 1a from the fluid supply nozzle 31 to the exhaust gas that has been subjected to the above-described primary exhaust gas treatment. Processing is performed.
That is, the fluid supply device 30 processes the air supplied by the air supply device 39 constituted by a blower or the like by the upstream fluid treatment device 1a having the configuration shown in FIG. Then, the ion-activated process air can be supplied and mixed with the exhaust gas at the supply section in the chimney.
As a result, the exhaust gas is strongly ionized by the processing air, so that oxygen (O) ionized with respect to, for example, carbon monoxide (CO) in the ionized exhaust gas strongly oxidizes this, and carbon dioxide Change to (CO ₂ ) and detoxify. Similarly, other harmful components are oxidized or reduced so that they are rendered harmless and sent downstream.

The upstream side fluid processing apparatus 1a of the illustrated example is a plate-shaped rotating member in which a net-type α-ray radiator 2 is formed in a vertical cylinder shape and is rotatably supported by a rotating shaft 42 of a motor 41 in the processing cylinder 4. 43 is detachably attached to the outer periphery of the processing cylinder 4 and an AC type magnetism generating section 6 is provided.
Thereby, when the fluid processing apparatus 1 passes the air supplied from the inflow port 14 through the rotating α-ray radiator 2 and sends it out from the outflow port 16, it is the same as that shown in the fourth embodiment of FIG. Further, the inside of the processing cylinder 4 is made into a kinetic active environment for air molecules by the magnetism generator 6, and the cylindrical α-ray radiator 2 is rotated in the processing cylinder 4, so that the α-ray radiator 2 is stirred while air is being stirred. Are crossed in a plurality of stages, and the contact between the air molecules and the α-rays is further promoted and the fluid is processed.

Further, as shown by a dotted line in FIG. 8, when the net-type α-ray radiator 2 is provided radially in the rotating cylindrical α-ray radiator 2, air molecules and α It is possible to perform fluid processing that further promotes contact with the wire and prevents processing leakage.
The upstream fluid processing apparatus 1a automatically cleans the cleaning fluid by injecting the cleaning fluid from the cleaning nozzle 44 installed on the side to the rotating cylindrical α-ray radiator 2 and cleaning the cleaned fluid. A maintenance structure for discharging the liquid from the drainage port 46 is provided.

  Next, the downstream side fluid treatment apparatus 1b according to the fifth embodiment that is installed on the most downstream side of the chimney and performs the tertiary exhaust gas treatment of the exhaust gas will be described. The downstream side fluid processing apparatus 1b is configured such that the processing cylinder 4 is formed in a drum shape larger than the diameter of the chimney, and an inflow pipe 27 that forms a downstream chimney is connected to the inlet 14 side, and the outlet 16 side is connected. An outflow pipe 28 forming an upstream chimney is connected. The processing cylinder 4 is provided with a net-type α-ray radiator 2 formed in a downward dish shape facing the inflow port 14 in the central portion, and the ultrasonic generator 7 above the central portion of the α-ray radiator 2. Is provided downward. Further, a net-shaped α-ray radiator 2 formed in a donut shape is provided on the inner periphery of the processing cylinder 4 so as to form a detour-like flow interval above the side of the dish-shaped α-ray radiator 2. Yes. Further, a panel type α-ray radiator 2 in which a plate-like body is coated with an α-ray radiation material is attached to the inner periphery of the processing cylinder 4.

In addition, an alternating-current magnetism generating unit 6 as a molecular motion promoting unit 3 different from the ultrasonic wave generating unit 7 is provided on the outer periphery of the processing cylinder 4 and the outer periphery of the end portion of the inflow pipe 27. Further, a permanent magnet type α-ray radiator 2 is installed on the lower surface of the dish-type α-ray radiator 2 as necessary.
The downstream fluid processing apparatus 1b having the above configuration activates the molecular motion of the exhaust gas supplied from the inlet 14 in the processing cylinder 4 by the molecular motion promoting unit 3. In an environment in which this molecular motion is activated, first, a fluid treatment is performed by the downward dish-shaped α-ray radiator 2, and then exhaust gas flowing out from the outer peripheral portion is fluid-treated by the upper α-ray radiator 2 without leaking, and a panel type Since the α-ray radiator 2 processes the exhaust gas along the inner wall of the processing cylinder, it is possible to complete the tertiary exhaust gas treatment and perform smooth discharge.

  The fluid treatment device 1 configured as described above includes a primary exhaust gas treatment for removing tar, and a secondary exhaust gas treatment (exhaust gas treatment air reforming) in which treated air fluid-treated by the α-ray radiator 2 is supplied to and mixed with the exhaust gas. Treatment) and tertiary exhaust gas treatment in which exhaust gas is passed through the α-ray radiator 2 in the processing cylinder 4 and irradiated with α-rays can be sequentially performed in the chimney. The fluid can be efficiently processed and discharged cleanly.

In the fluid processing, the fluid supply device 30 including the upstream fluid processing device 1a forcibly supplies the processing air into the large diameter processing tube 4 installed on the downstream side. Thus, exhaust gas treatment can be more reliably promoted by sufficiently mixing with exhaust gas. Further, the contamination of the α-ray radiator 2 and the inner wall in the processing cylinder 4 can be suppressed, the apparatus can be simplified and the maintenance work can be saved.
In this embodiment, the processing fluid processed by the upstream fluid processing device 1a is supplied to the fluid flowing through the frame 4 of the downstream fluid processing device 1b and mixed in this supply section to perform fluid processing. The installation of the α-ray radiator 2 in the cylinder 4 can be made unnecessary, and the apparatus can be simplified and the maintenance work can be saved without contaminating the α-ray radiator 2.

In addition, when the exhaust gas treatment by the fluid supply device 30 is sufficient, the α-ray radiator 2 and the magnetism generating unit 6 of the treatment cylinder 4 can be omitted.
Furthermore, when the exhaust gas treatment apparatus 1a is provided with a mist supply pipe 23 as necessary, it is possible to additionally perform a mist treatment similar to that of the above-described embodiment, and it is possible to further promote cleaning according to the situation of the exhaust gas. . If the processing cylinder 4 is provided with a cleaning device similar to that of the upstream fluid processing device 1a and the cleaning liquid is sprayed from a cleaning nozzle (not shown), maintenance work can be saved.
In addition to the exhaust gas treatment, the fluid treatment apparatus 1 can effectively perform deodorization and purification of indoor air such as food processing or livestock barns and factories, and increase in the amount of oxygen. In this case, outside air is taken in and supplied to the inside of the cylindrical portion in which the installation of the burner device 36 and the downstream fluid processing device 1b is omitted, and the indoor air is supplied to the upstream fluid processing device 1a. desirable.

  Next, with reference to FIG. 9, FIG. 10, the fluid processing apparatus 1 concerning 6th Embodiment and its usage example are demonstrated. When the fluid processing apparatus 1 is provided as described above in the fuel piping system 12b of the engine 12 in the third embodiment shown in FIG. 4, it can be used as a liquid processing apparatus for fuel reforming. In this example, the processing cylinder 4 is a pipe having a circular cross section, and the α-ray radiator 2 to be installed is the same as that shown in the above-mentioned Patent Document 1, with a large number of granular bodies (hereinafter referred to as α 2a). Among the fluids passing through the fluid processing apparatus 1 having the above-described configuration, oils can be activated and prevented from being deteriorated by receiving a strong ionization action by a large number of α-ray granular radiators 2a. Can improve combustion efficiency by making small molecules and radicals by breaking carbon molecular bonds, and can also clean exhaust gas.

In the illustrated fluid processing apparatus 1, the α-ray granular radiator 2 a and a disk net separator 47 that partitions and holds a predetermined amount of the α-ray granular radiator 2 a in the processing cylinder 4 are inserted into the processing cylinder 4. In the state, a lid 48 having a plurality of flow holes 48 a is provided at the inlet 14 and the outlet 16. In addition, the molecular motion promoting unit 3 has a configuration in which an AC type magnetism generating unit 6 is provided at least at a downstream position on the outer periphery of the processing cylinder 4.
The inflow pipe 27, which is a fuel pipe, is connected to the right lid 48 via a joint 49, and the delivery pipe 28 is connected to the left lid 48 via a joint 49. The fuel pipe including the fluid processing apparatus 1 shown in FIG. Configure the system.

  In the above configuration, the plurality of separators 47 define a plurality of processing chambers in the processing cylinder 4 by supporting the central portion of the rod-shaped core material 51 with a predetermined interval. Further, by inserting a predetermined number of α-ray granular radiators 2a corresponding to the space in each processing chamber, a moving space in which each α-ray granular radiator 2a moves freely is formed, and clogging is prevented from occurring. Increase in resistance is suppressed. Further, when the fuel oil flows downstream, the α-ray granular radiators 2a in the processing chambers are dammed by the separators 47 and are movably accumulated, and are restricted from moving toward the adjacent processing chambers. .

  Then, a space (space) is reliably formed between the upstream separator 47 and the lid 48 in a state where the α-ray granular radiator 2a is moved and accumulated on the downstream side based on the flow of the fluid. The flow resistance of the fuel oil can be reduced as compared with the case where a large amount of the α-ray granular radiator 2a is put in without providing the separator 47 in 4. Therefore, even when the processing cylinder 4 is formed long and a large amount of the α-ray granular radiator 2a is inserted, the fluid processing performance can be improved without hindering the flow of the fuel oil.

  Further, since each α-ray granular radiator 2a freely moves in each processing chamber due to the flow and vibration of the fuel oil, the circulating fuel oil has sufficient surface contact with each α-ray granular radiator 2a. Promote fluid treatment by Furthermore, since the fuel oil treatment is further promoted in an environment in which the molecular motion of the fuel oil by the magnetic generator 6 is activated, it is possible to improve the combustion efficiency of the fuel oil and further reduce harmful substances in the exhaust gas. it can.

  Further, the fluid processing apparatus 1 is provided with a fluid supply nozzle 31 similar to that described above on the outer periphery of the processing cylinder 4, so that air or the like can be easily supplied to an appropriate place in the processing cylinder 4. The fluid supply nozzle 31 is desirably provided close to the downstream side of the upstream separator 47. In this case, air can be supplied to the upstream side of the processing chamber, so that α is integrated on the downstream side. Without being hindered by the linear radiator 2a, it is possible to mix the treated air that has been fluid-treated with the fuel oil.

The air-mixed fuel oil in which the processing air is mixed with the fuel oil has a surface on the plurality of α-ray granular radiators 2a when passing through a complicatedly refracted small gap formed by accumulation of the α-ray radiators 2 on the downstream side. Since fluid treatment by α-ray irradiation is repeated while in contact, it is possible to obtain a reformed fuel oil containing finer bubbles (nanobubbles).
When the reformed fuel oil treated in this way is supplied to the engine 12, the combustion efficiency can be further increased, and harmful substances in the exhaust gas and fuel consumption can be reduced.

The core material 51 can also be configured to be used as the permanent magnet type magnetism generator 6. In this case, the magnetic force at the center of the processing cylinder 4 can be easily supplemented. The generation unit 6 can be downsized. When the AC magnetic generator 6 is not used, if the core 51 or the separator 47 is the permanent magnet generator 6, fluid processing can be performed with a simpler and cheaper configuration. Further, in the central portion on the downstream side of the α-ray radiator 2, for example, when a flow regulating plate 52 that partially regulates the flow is provided in the core material 51 or the flow hole 48 a in the central portion of the separator 47 is made small in diameter, Can be made to contact the α-ray radiator 2 uniformly while suppressing local outflow.

Further, in the fluid processing apparatus 1 of the illustrated example, the α-ray radiator 2 is an α-ray granular radiator 2a made up of a number of granular materials, but as shown in FIG. The net-type or sheet-type (plate-like) α-ray radiator 2 can be used.
That is, the α-ray radiator 2 shown in FIG. 10 (A) forms a predetermined distribution interval in the cross-sectional direction of the processing cylinder 4 by rolling a sheet-type one having an α-ray emitting material on the surface into a spiral shape. Inserted. Further, the α-ray radiator 2 may be a net-type having a predetermined length and formed into a plurality of large and small cylindrical shapes, and may be inserted and held together with a predetermined flow interval in the cross-sectional direction of the processing tube 4.

  The α-ray radiator 2 shown in FIG. 10 (B) is formed by forming a plurality of unit processing chambers having a predetermined length along the flow direction in the cross-sectional direction by using the same net type or sheet type as described above. It is provided in a honeycomb shape when viewed from the distribution direction. According to this, fluid processing can be efficiently performed even in the large-diameter processing cylinder 4 in a state of being divided for each unit processing chamber. In addition, when the unit processing chamber is added to the plate-like body by twisting, tilting or curved surfaces in the flow direction, the fluid flowing through the unit processing chamber can be brought into direct contact with the α-ray radiation material, and the length of the unit processing chamber can be increased. By shortening, it is possible to reduce the size of the apparatus and save the α-ray radiation material.

Furthermore, if the unit processing chambers having inclinations and twists intersecting the flow direction in the plate-like body are arranged in the flow direction opposite to each other, a vortex can be formed and sent out from the most downstream side.
In addition, a plurality of processing cylinders 4 configured as described above can be easily connected via a connecting pipe (not shown), and a fluid can be processed according to the purpose over a long distance. Therefore, the fluid processing performance required by various utilization devices can be manufactured at a low cost with a highly productive configuration. In addition, it is possible to easily install additional structures such as the mist supply pipe 23, the fluid supply nozzle 31, the molecular motion promoting portion 3 and the like in the connection pipe.

  Further, when the fluid is processed over a long distance as described above, a long pipe or hose (not shown) is used as the processing cylinder 4, and the aforementioned α-ray granular radiator 2a or various α-ray radiators 2 are placed therein. Can be processed. In this case, the long processing cylinder 4 can be bent by selecting the length and diameter in any shape, so that it is easy to perform fluid processing according to various purposes and installation in the utilization device. . Further, for example, if the processing tube 4 is made of a flexible hose and the α-ray granular radiator 2a is inserted, it becomes easy to spirally wind around a column member having a circular cross section or an arbitrary cross section, and the fluid is made into a long spiral path. Since it is moved along, efficient fluid treatment can be promoted for various gases. Further, there is an advantage that the structure of the fluid processing apparatus 1 can be saved in space and can be manufactured at low cost.

In addition, the fluid processing apparatus 1 of the said embodiment can be used simply and cheaply not only for fuel oil but also for dirty oil and waste oil purification treatment, edible oil reforming and the like.
When water is fluid-treated by the fluid treatment device 1 having the above-described configuration, water molecules are repeatedly irradiated with α rays while passing through each α-ray granular radiator 2a in an aggregated state, so that the treated water is excessive. Generation of hydrogen oxide (H ₂ O ₂ ) and H ⁺ + OH ⁻ ions are efficiently generated.
Therefore, when the modified product water is supplied to plants and garden trees by means such as spraying, it acts on bacteria and pathogens and is sterilized by the stabilization reaction of H ⁺ or OH ^- ions, so there is no need for a disinfectant. Can be suppressed, and the natural healing power of plants can be increased .

That is, according to this generated water, it is possible to rationally grow and cultivate crops that suppress the use of disinfectants, as well as washing hands, excrement, cleaning cutting tools such as cutting boards, and preventing mold generation. It can be carried out. In addition, sterilization and washing that are friendly to the human body and the environment, without relying on harmful disinfectants and detergents, can be quickly and inexpensively installed in nosocomial infection prevention fields such as noroviruses, food processing facilities, or water purification facilities. be able to.

Furthermore, the fluid processing apparatus 1 having the configuration of the embodiment is filled with a large number of ceramic granules (hereinafter referred to as hard balls) in which the α-ray coating is omitted in place of the α-ray granular radiator 2a. Can also be used. That is, the hard ball in this case is shown in Patent Document 1, in which the ceramic material of the inner layer is mainly composed of barley stone powder, quartz powder and titanium oxide powder as ferroelectrics showing piezoelectricity, and silicic acid as binder It is desirable to be a hard ceramic granule that is formed by adding and mixing aluminum compound powder or the like to form a granule having a required shape and size and then firing.

As a result, the fluid processing apparatus 1 containing a large number of hard balls having a piezoelectric phenomenon causes the electric force generated in the hard balls due to the collision force with which the hard balls contact each other due to the flow of water and the friction with which the surfaces contact with water. results discharge are repeated indefinitely, the water molecules H ⁺ + OH ^- that turn into ions. In addition, it is possible to easily produce good water that has been decomposed and eliminated carcinogenic harmful substances such as chlorine contained in tap water.

  Therefore, the fluid processing apparatus 1 having a hard ball as an application apparatus for fluid processing water does not generate hydrogen peroxide unlike the α-ray granular radiator 2a, and can be activated at low cost even with tap water. Therefore, it can be easily installed and optimized in each household water supply, commercial water supply, water treatment, hot spring, etc. The fluid processing apparatus 1 has the processing cylinder 4 installed in the vertical direction, and when the fluid is supplied against the dead weight of the hard ball from the lower side, the function of the hard ball is further exerted to promote the fluid processing. There are features such as.

Moreover, since the said produced water does not make calcium ion adhere in a pipe line, it can be used cheaply as boiler water which is hard to attach a scale. Further, the fluid processing apparatus 1 can be used by simply incorporating it in a required portion of the boiler.
Moreover, it is easy to supply and mix air in the middle of the treatment cylinder 4, and it is possible to easily and inexpensively produce bubble-containing active water having high ion activity and containing fine bubbles. As a result, it is possible to easily supply the bubble-containing active water together with the fuel to various combustion apparatuses, and to improve the interfacial activity, the mixing ratio with the fuel is increased, emulsification is completed, and combustion is facilitated. Accordingly, it is possible to promote fuel saving and exhaust gas purification while achieving complete combustion.

Furthermore, as shown in the above embodiments, the fluid treatment apparatus 1 having the α-ray radiator 2 or the α-ray granular radiator 2a uses CO ₂ as an effective resource as well as a device that reduces CO ₂ in the exhaust gas. Means and methods are also readily available. That is, since the fluid treatment apparatus 1 makes α rays contact with CO ₂ in the exhaust gas, CO ₂ can be easily decomposed into O + CO. Then, the decomposed CO is fixed using a catalyst, and α-rays are again brought into contact with the fixed CO to be decomposed into C + O, and C is stabilized to C ₂ using a catalyst and recovered.

Next, H ₂ is mixed with the recovered C ₂ , and α-rays are brought into contact with each other in the catalyst to produce a hydrocarbon compound. As described above, by using the fluid treatment device 1 to reduce or recover CO ₂ , the exhaust gas can be changed to fuel or a fuel increasing agent, so that global warming can be prevented by simple and economical means. There are features such as being able to contribute greatly.
The CO ₂ treatment by the fluid treatment apparatus 1 is not limited to exhaust gas flowing through a chimney or an exhaust pipe, and can be easily used for various CO ₂ reduction countermeasures by preventing the apparatus from becoming large.

It is a perspective view which shows the structure which provided the fluid processing apparatus of this invention in the motor vehicle engine. It is sectional drawing which shows the structure of the fluid processing apparatus in connection with 1st Embodiment of this invention. It is sectional drawing which shows the structure of the fluid processing apparatus in connection with 2nd Embodiment of this invention. It is sectional drawing which shows the structure of the fluid processing apparatus in connection with 3rd Embodiment of this invention. It is sectional drawing which shows the structure of the fluid processing apparatus in connection with 4th Embodiment of this invention. (A) is the sectional view on the AA line of FIG. (B) is the BB sectional view taken on the line of FIG. (C) is CC sectional view taken on the line of FIG. It is sectional drawing which shows the structure of the fluid processing apparatus in connection with 5th Embodiment of this invention. FIG. 6 is a cross-sectional plan view showing the configuration of the fluid supply device in FIG. 5. It is sectional drawing which shows the structure of the fluid processing apparatus in connection with 6th Embodiment of this invention. FIG. 9A is a cross-sectional view showing a state in which a net-type α-ray emitter is rounded, showing another embodiment of the α-ray emitter installed in the processing cylinder of FIG. 9. (B) is sectional drawing which shows the structure of the alpha ray emitter formed in the shape of a beehive.

DESCRIPTION OF SYMBOLS 1 Fluid processing apparatus 1a Another fluid processing apparatus 2 alpha ray radiator 2a alpha ray granular radiator 3 molecular motion promotion part 4 frame (processing cylinder)
7 Ultrasonic generator 14 Inlet 16 Outlet 17 Filter 23 Mist supply pipe 31 Fluid supply nozzle 36 Burner equipment

Claims (7)

An α-ray emitter (2) provided with an α-ray emitting material that emits α-rays inside a frame (4) having an internal space as a fluid flow path from the inlet (14) toward the outlet (16) In the fluid processing apparatus (1) for performing fluid processing by irradiating the fluid with alpha rays and ionizing the fluid, the frame (4) activates the molecular motion of the fluid (3) A filter in which the fluid subjected to molecular motion activation by the molecular motion promoting portion (3) is irradiated with α-rays to perform fluid treatment, and the α-ray radiator (2) is provided in the frame (4) ( 17) provided upstream of or downstream of the fluid processing device (1), the fluid processing device (1) is installed in the exhaust passage of the combustion device (35), and the fluid processing device (1) is installed in the exhaust passage. Provided with a fluid treatment device (1a) and a downstream fluid treatment device (1b) connected to the exhaust passage, The delivery port (16) of the fluid treatment device (1a) is connected to the frame (4) of the downstream fluid treatment device (1b), and the treatment fluid subjected to fluid treatment by the upstream fluid treatment device (1a) is treated as downstream fluid treatment. While supplying the fluid flowing through the frame (4) of the apparatus (1b), high-temperature energy is introduced into the exhaust passage upstream of the supply section to which the processing fluid is supplied to the downstream fluid processing apparatus (1b). A fluid treatment device provided with a burner device (36) for supplying .   The α-ray radiator (2) is an α-ray granular radiator (2a) made of a granular material coated with an α-ray radiation material, and a number of α-ray granular radiators (2a) are moved into the frame (4). The fluid processing apparatus according to claim 1, wherein the fluid processing apparatus is configured to be filled with fluid.   The fluid processing apparatus according to claim 1 or 2, wherein the α-ray radiator (2) is rotatably supported in the frame (4).   The fluid processing apparatus according to claim 1, 2 or 3, wherein the molecular motion promoting unit (3) is an ultrasonic wave generating unit (7) that generates ultrasonic waves toward the α-ray emitter (2).   The fluid processing apparatus according to claim 1, 2, 3, or 4, wherein the molecular motion promoting unit (3) is a magnetic generation unit (6) that generates magnetic field lines toward the α-ray emitter (2).   The fluid processing apparatus according to claim 1, 2, 3, 4, or 5, wherein a fluid supply nozzle (31) that supplies another fluid to the fluid that circulates inside the frame body (4).   The mist supply pipe (23) for supplying mist to the frame (4) on the upstream side or the downstream side of the α-ray radiator (2) with respect to the fluid flowing inside the frame body (4). Or 5 or 6 fluid processing apparatus.

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